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    • 11. 发明专利
    • Exhaust gas disposal method using alternating combustion type hot air burner
    • 使用替代燃烧式热空气燃烧器的排气处理方法
    • JP2003021324A
    • 2003-01-24
    • JP2001203288
    • 2001-07-04
    • Babcock Hitachi Kkバブコック日立株式会社
    • KATSUTA YASUTSUNENOMURA SHINICHIROBABA AKIRAHANAYAMA FUMIHIKOTAKARAYAMA NOBORUKUMAGAI KENJI
    • F23L15/02F23G7/06
    • Y02E20/348
    • PROBLEM TO BE SOLVED: To provide an exhaust gas disposal method using an alternating combustion type hot air burner, which can reduce uncombusted components, especially, CO within exhaust gas.
      SOLUTION: This exhaust gas disposal method is provided with two systems burning. A gas containing noxious components and fuel is supplied to a main burner of one system so as to pyrolyze the noxious components and recovering and a heat accumulator of the other system accumulates heat of pyrolized produced gas an accumulator of the one system recoveres and accumulates heat of the pyrolized produced gas. When the burner of the other system pyrolizes the noxious components. This exhaust gas disposal operation is repeated to accumulate the heat of the pyrolized gas produced by the burner in combustion in the heat accumulator of the burner in stoppage of combustion for use as a heat source at the next combustion. The supply of fuel to the burner in pyrolisis of the noxious components is stopped prior to the changeover of the burner when switching the burner for pyrolizing the noxious components by the changeover of a gas passage.
      COPYRIGHT: (C)2003,JPO
    • 要解决的问题:提供一种使用交替燃烧式热空气燃烧器的排气处理方法,其可以减少排气中的未燃组分,特别是CO。 解决方案:这种废气处理方法设有两个系统燃烧。 将含有有害成分和燃料的气体供给到一个系统的主燃烧器,以便对有害成分进行热解并回收,另一个系统的蓄热器累积热解生成气体的热量,一个系统的蓄能器回收并积累 热解产生的气体。 当其他系统的燃烧器加热有毒成分时。 重复这种排气处理操作,以在燃烧器的蓄热器燃烧时在燃烧器中燃烧时产生的热解气体的热量在燃烧中累积,以在下一次燃烧时用作热源。 在切换燃烧器之前,在燃烧器切换燃烧器之前,通过气体通道的转换来停止对燃烧器供应燃烧器,以便在燃烧器转换时对燃烧器进行热解。
    • 16. 发明专利
    • METHOD OF GASIFYING COAL-WATER SLURRY
    • JPS63135490A
    • 1988-06-07
    • JP28296186
    • 1986-11-27
    • BABCOCK HITACHI KK
    • HANAYAMA FUMIHIKOKIDA EIJI
    • C10J3/46C10J3/00
    • PURPOSE:To attain effective utilization of by-product gypsum and stable flow- down of intra-gasifier oven slag, by mixing by-product gypsum sludge with a high-temp. gas to elevate the temp. of the sludge, thereby realizing a high- temp. slurry form, and feeding the slurry to a high-temp. region at the lower portion of a gasifier oven so as to incorporate it into the slag within the oven. CONSTITUTION:The following five steps are employed: (1) a step of oxidizing a coal-water slurry 1 in a desulfurization reactor 2, (2) a step of separating the product from the desulfurization reactor 2 in a thickener 5 into a thick desulfurized coal-water slurry 7 and a supernatant of dil. sulfuric acid, (3) a step of feeding the desulfurized coal-water slurry 7 mixed with a gasifying agent 8 into a gasifier oven 12, (4) a step of mixing the remaining dil. sulfuric acid with limestone 4 in a mixing tank 9 under agitation so as to effect neutralization and separating the deposit, by means of a gypsum thickener 10, into a thick gypsum sludge 11 and a supernatant, and (5) a step of mixing the gypsum sludge 11 with a high-temp. gas 20 (discharge gas from the desulfurization reactor 2) to elevate the temp. of the sludge and feeding the sludge to the high temp. region at the lower portion of the gasifier oven 12 so as to incorporate it into the slag within the oven 12.
    • 17. 发明专利
    • Gasification furnace, gasification power generation plant, gasification apparatus and method for operating gasification furnace
    • 气化炉,气化发电厂,气化装置及运行气化炉的方法
    • JP2013007059A
    • 2013-01-10
    • JP2012223903
    • 2012-10-09
    • Babcock Hitachi Kkバブコック日立株式会社Electric Power Dev Co Ltd電源開発株式会社
    • ISHIGA TAKUYAKISO FUMIHIKOAKIYAMA TORUHANAYAMA FUMIHIKOARIMORI EIJIYAMASHITA HIROSHI
    • C10J3/46
    • Y02E20/18Y02P20/124
    • PROBLEM TO BE SOLVED: To provide a gasification furnace designed to suppress degradation in energy efficiency by ensuring a slag tap to be kept hot without charging a quenching section with any auxiliary fuel, and also to keep a lower face of the slag tap hot with a small amount of gas to achieve a stable slag downflow, and to provide a gasification power generation plant and a gasification device.SOLUTION: A nozzle or a burner is horizontally installed at a position just below a slag tap in a quenching section, and a gas containing oxygen but containing no fuel is supplied through the nozzle or the burner to collide with a wall face of the quenching section. Alternatively, multiple nozzles or burners are made to oppose to each other and jet streams of an oxygen-containing gas supplied by the nozzles or the burners are collided with each other in the quenching section. Thereby, in the quenching section, a rising gas flow toward a lower face of the slag tap is generated. The oxygen-containing gas supplied into the quenching section is mixed with a generated gas descending from a gasification section through the slag tap near the lower face of the slag tap and burnt to keep the lower face of the slag tap hot.
    • 要解决的问题:提供一种气化炉,其旨在通过确保炉渣丝保持热而不用任何辅助燃料充入淬火部分,并且还保持炉渣抽头的下表面来抑制能量效率的降低 热量少量气体达到稳定的炉渣下流,并提供气化发电厂和气化装置。 解决方案:喷嘴或燃烧器水平地安装在淬火部分中渣柱正下方的位置,并且含氧但不含燃料的气体通过喷嘴或燃烧器供应以与 淬火部分。 或者,使多个喷嘴或燃烧器彼此相对,并且由喷嘴或燃烧器供应的含氧气体的喷流在淬火部分中相互碰撞。 因此,在淬火部中,产生朝向炉渣龙头的下面的上升的气体流。 供给到淬火部的含氧气体与从气化部通过炉渣龙头下面的炉渣分离器下降的产生的气体混合并燃烧,以使炉渣的下表面变热。 版权所有(C)2013,JPO&INPIT
    • 18. 发明专利
    • Two-stage gasification furnace
    • 两级气化炉
    • JP2008231294A
    • 2008-10-02
    • JP2007074287
    • 2007-03-22
    • Babcock Hitachi KkElectric Power Dev Co Ltdバブコック日立株式会社電源開発株式会社
    • KOYAMA SHUNTAROSUZUKI HIDEKISOTOOKA MASAOARIMORI EIJIAKIYAMA TORUHANAYAMA FUMIHIKO
    • C10J3/46C10J3/50
    • PROBLEM TO BE SOLVED: To form desired temperature distribution by clearly forming a low temperature area and a high temperature area in a furnace body without meaninglessly making height of the furnace body high when a diameter of the furnace body is increased for the purpose that a two-stage gasification furnace is scaled-up, to prevent damage of a furnace wall, and to reduce heat loss from the furnace wall.
      SOLUTION: The two-stage gasification furnace is provided with the cylindrical furnace body 2, an upper burner group 3 arranged on an upper part of the furnace body, and a lower burner group 4 arranged on a lower part of the furnace body. On an upper end of the furnace body 2, a gas outlet 5 for discharging a product gas is formed, and on a lower end of the furnace body 2, a molten slag outlet 7 for discharging a molten slag is formed. In the gasification furnace, a ratio of a clearance Lb of the upper burner group 3 and the lower burner group 4 and a clearance Lu of the gas outlet 5 and the upper burner group 3 is made to Lb/Lu=2-12.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题为了在炉体的直径增加的同时,通过在炉体中清楚地形成低温区域和高温区域而不会使炉体的高度无意义地变高而形成所需的温度分布 两级气化炉被放大,以防止炉壁的损坏,并减少炉壁的热损失。 解决方案:两级气化炉设置有圆筒形炉体2,布置在炉体上部的上燃烧器组3和设置在炉体下部的下燃烧器组4 。 在炉体2的上端形成有用于排出产品气体的气体出口5,在炉体2的下端形成用于排出熔渣的熔渣出渣口7。 在气化炉中,上燃烧器组3和下燃烧器组4的间隙Lb与气体出口5和上燃烧器组3的间隙Lu的比率为Lb / Lu = 2-12。 版权所有(C)2009,JPO&INPIT